EP1529788B1 - Method for manufacturing a composite tire of polyurethane tread and radial carcase - Google Patents
Method for manufacturing a composite tire of polyurethane tread and radial carcase Download PDFInfo
- Publication number
- EP1529788B1 EP1529788B1 EP04019085A EP04019085A EP1529788B1 EP 1529788 B1 EP1529788 B1 EP 1529788B1 EP 04019085 A EP04019085 A EP 04019085A EP 04019085 A EP04019085 A EP 04019085A EP 1529788 B1 EP1529788 B1 EP 1529788B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- polyurethane
- polymer
- rubber body
- tread
- particles
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Not-in-force
Links
- 229920002635 polyurethane Polymers 0.000 title claims abstract description 72
- 239000004814 polyurethane Substances 0.000 title claims abstract description 72
- 239000002131 composite material Substances 0.000 title claims abstract description 28
- 238000000034 method Methods 0.000 title claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 9
- 229920001730 Moisture cure polyurethane Polymers 0.000 claims abstract description 109
- 229920001971 elastomer Polymers 0.000 claims abstract description 101
- 239000005060 rubber Substances 0.000 claims abstract description 101
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 42
- 239000003795 chemical substances by application Substances 0.000 claims description 30
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 27
- 229910052799 carbon Inorganic materials 0.000 claims description 27
- 239000002105 nanoparticle Substances 0.000 claims description 27
- 239000012298 atmosphere Substances 0.000 claims description 25
- -1 polytetramethylene Polymers 0.000 claims description 24
- 239000000203 mixture Substances 0.000 claims description 23
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titanium dioxide Inorganic materials O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 23
- 239000002245 particle Substances 0.000 claims description 22
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims description 21
- 239000003292 glue Substances 0.000 claims description 19
- 239000007787 solid Substances 0.000 claims description 18
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 17
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 16
- 229920002121 Hydroxyl-terminated polybutadiene Polymers 0.000 claims description 15
- 229920001228 polyisocyanate Polymers 0.000 claims description 15
- 239000005056 polyisocyanate Substances 0.000 claims description 15
- UPMLOUAZCHDJJD-UHFFFAOYSA-N 4,4'-Diphenylmethane Diisocyanate Chemical compound C1=CC(N=C=O)=CC=C1CC1=CC=C(N=C=O)C=C1 UPMLOUAZCHDJJD-UHFFFAOYSA-N 0.000 claims description 11
- 239000004094 surface-active agent Substances 0.000 claims description 11
- 239000012948 isocyanate Substances 0.000 claims description 9
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 claims description 9
- 150000002513 isocyanates Chemical class 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 8
- 229920005862 polyol Polymers 0.000 claims description 8
- 150000003077 polyols Chemical class 0.000 claims description 8
- 239000006087 Silane Coupling Agent Substances 0.000 claims description 7
- SBJCUZQNHOLYMD-UHFFFAOYSA-N 1,5-Naphthalene diisocyanate Chemical compound C1=CC=C2C(N=C=O)=CC=CC2=C1N=C=O SBJCUZQNHOLYMD-UHFFFAOYSA-N 0.000 claims description 5
- 239000011248 coating agent Substances 0.000 claims description 5
- 238000000576 coating method Methods 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 5
- WTPYFJNYAMXZJG-UHFFFAOYSA-N 2-[4-(2-hydroxyethoxy)phenoxy]ethanol Chemical compound OCCOC1=CC=C(OCCO)C=C1 WTPYFJNYAMXZJG-UHFFFAOYSA-N 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims 3
- 238000001035 drying Methods 0.000 claims 2
- 238000010298 pulverizing process Methods 0.000 claims 2
- 238000009966 trimming Methods 0.000 claims 2
- 238000005096 rolling process Methods 0.000 abstract description 8
- 238000011109 contamination Methods 0.000 abstract description 6
- 230000007613 environmental effect Effects 0.000 abstract description 6
- 238000000465 moulding Methods 0.000 description 34
- 244000043261 Hevea brasiliensis Species 0.000 description 11
- 229920003052 natural elastomer Polymers 0.000 description 11
- 229920001194 natural rubber Polymers 0.000 description 11
- 150000002009 diols Chemical class 0.000 description 5
- 239000000654 additive Substances 0.000 description 3
- 239000012299 nitrogen atmosphere Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- FCIIEZYZYBGUBJ-UHFFFAOYSA-N 2-ethyl-1-propyl-1-trimethoxysilylhydrazine Chemical compound CCNN(CCC)[Si](OC)(OC)OC FCIIEZYZYBGUBJ-UHFFFAOYSA-N 0.000 description 2
- 239000010692 aromatic oil Substances 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000020169 heat generation Effects 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- DNKJROPZENRHBM-UHFFFAOYSA-N n-[2-[diethoxy(propyl)silyl]oxyethyl]benzamide Chemical compound CCC[Si](OCC)(OCC)OCCNC(=O)C1=CC=CC=C1 DNKJROPZENRHBM-UHFFFAOYSA-N 0.000 description 1
- 229920005906 polyester polyol Polymers 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 229920003225 polyurethane elastomer Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003878 thermal aging Methods 0.000 description 1
- DVKJHBMWWAPEIU-UHFFFAOYSA-N toluene 2,4-diisocyanate Chemical compound CC1=CC=C(N=C=O)C=C1N=C=O DVKJHBMWWAPEIU-UHFFFAOYSA-N 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000010920 waste tyre Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
- C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
- C08G18/7657—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
- C08G18/7678—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing condensed aromatic rings
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29D—PRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
- B29D30/00—Producing pneumatic or solid tyres or parts thereof
- B29D30/06—Pneumatic tyres or parts thereof (e.g. produced by casting, moulding, compression moulding, injection moulding, centrifugal casting)
- B29D30/52—Unvulcanised treads, e.g. on used tyres; Retreading
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
- B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
- B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
- B60C1/0016—Compositions of the tread
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
- C08G18/12—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step using two or more compounds having active hydrogen in the first polymerisation step
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4854—Polyethers containing oxyalkylene groups having four carbon atoms in the alkylene group
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/67—Unsaturated compounds having active hydrogen
- C08G18/69—Polymers of conjugated dienes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/67—Unsaturated compounds having active hydrogen
- C08G18/69—Polymers of conjugated dienes
- C08G18/698—Mixtures with compounds of group C08G18/40
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J175/00—Adhesives based on polyureas or polyurethanes; Adhesives based on derivatives of such polymers
- C09J175/04—Polyurethanes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2075/00—Use of PU, i.e. polyureas or polyurethanes or derivatives thereof, as moulding material
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2380/00—Tyres
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/04—Carbon
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
- C08K3/36—Silica
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K9/00—Use of pretreated ingredients
- C08K9/04—Ingredients treated with organic substances
- C08K9/06—Ingredients treated with organic substances with silicon-containing compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2666/00—Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
- C08L2666/54—Inorganic substances
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/80—Technologies aiming to reduce greenhouse gasses emissions common to all road transportation technologies
- Y02T10/86—Optimisation of rolling resistance, e.g. weight reduction
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S264/00—Plastic and nonmetallic article shaping or treating: processes
- Y10S264/77—Processes of molding urethanes
Definitions
- the present invention relates to a method for manufacturing a composite rubber tire, and more particularly to a composite rubber tire that has a polyurethane tread to achieve an environmentally friendly tire with excellent mechanical efficiency.
- Environmentally friendly tires mostly refer to radial tires that have less rolling resistance to reduce vehicles fuel consumption and exhaust, and to reduce the waste gas ejected. By using environmentally friendly tires, rolling resistance is reduced by 22-25%, and fuel consumption is reduced by 3-8%. Therefore, research into environmentally friendly tires is a popular subject for tire manufacturers worldwide.
- Natural rubber radial tires have an internal body and an outer surrounding layer. The internal body and the outer layer are made of natural rubber.
- the natural rubber radial tires have excellent kinetic properties such as low heat generation and good flexibility and are suitable for use as high-speed tires.
- Natural rubber radial tires usually are coated with an improving glue on the outer surface to reduce the rolling resistance and to strengthen the tires.
- Current third generation radial tires have a rolling resistance 30 % less than first generation radial tires.
- nature rubber tires still have the following drawbacks:
- the natural rubber radial tires are not actually environmentally friendly.
- manufacturers have started to focus on using non-pollutants and apply a new improving glue on the tire to reduce rolling resistance. Furthermore, the manufacturers also want to increase the wear-resistance of the tire to improve tire durability to reduce the quantity of waste tires and to reduce heavy metal pollutants released into the environment.
- Molded polyurethane tires have an internal body and an outer surrounding layer.
- the internal body and the outer layer are made of polyurethane.
- the polyurethane tire has excellent wear-resistance that makes the tire durable and overcomes the problem of an excessive number of discarded tires. Furthermore, the polyurethane tire is very strong and does not need either carbon black or aromatic oil as additives. Therefore, the polyurethane tire has no environmental problems caused by the additives.
- the polyurethane tire still has the following drawbacks.
- the present invention intends to mitigate or obviate the disadvantages of the conventional environmental friendly tire.
- the main objective of the present invention is to provide a method for manufacturing a composite rubber tire with a polyurethane tread.
- the another main objective of the present invention is to provide a composite rubber tire with a polyurethane tread that has excellent flexibility, low rolling-resistance, high oil-saving efficiency and excellent durability.
- a method for preparing a composite rubber tire with a polyurethane tread in accordance with the present invention where the composite rubber tire has an internal rubber body with an outer surface and a polyurethane tread comprises the following steps:
- the internal rubber body is optionally a radial rubber tire or a bias-ply rubber tire to serve as a radial carcass and has an intermediate glue layer.
- the intermediate glue layer is laminated on the outer surface of the internal rubber body when the internal rubber body is molded. Then, the intermediate glue layer is vulcanized and trimmed at surfaces to be coated with the polyurethane pre-polymer.
- the polyurethane pre-polymer is made in a "low polymerized polyol and isocyanate" system, which indicates the pre-polymer is synthesized by low polymerized polyol and isocyanate.
- the "low polymerized polyol and isocyanate" system is selected from a system A or a system B.
- System A is a "polytetramethylene glycol and 1,5-naphthalene diisocyanate" system.
- the polytetramethylene glycol has a molecular weight of 1000 to 3000.
- a chain-extending agent is a low molecular diol and has a chain-extending coefficient of 0.95 to 0.98.
- System B is a "hydroxyl-terminated polybutadiene and 4,4'-diphenylmethane diisocyanate" system.
- the hydroxyl-terminated polybutadiene has a molecular weight of 1000 to 2000.
- a chain-extending agent is a low molecular weight diol and has a chain-extending coefficient of 0.95 to 0.98.
- the low polymerized polyol is held in a -0.095 to -0.098 MPa vacuum atmosphere to dehydrate at 120 to 140° C for 2 to 3 hours and then cools down to 60°C.
- Isocyanate is then added to the low polymerized polyol to react in a -0.095 to -0.098 MPa vacuum atmosphere at 70 to 80°C for 1 to 2 hours to achieve the polyurethane pre-polymer.
- the quantity of isocyanate is controlled to make the isocyanate group content 5.0 to 6.0 percent of the total polyurethane pre-polymer.
- the quantity detection of isycyanate is popular in stoichiometry and redundant description is obviated here.
- the step of improving the polyurethane pre-polymer (3) modifies the polyurethane pre-polymer by treating the polyurethane pre-polymer with surface-treated nano-TiO 2 particles.
- Nano-TiO 2 particles 10 to 40 nm in diameter are activated by heating and mixed well with an ethanol solution containing a silane coupling agent.
- the silane coupling agent in the ethanol solution is 30 to 50 wt % of the weight of nano-TiO 2 particles.
- the ethanol solution is 3 to 5 times the silane coupling agent.
- the mixture is heated to 220 to 240° C and dried for 4 to 6 hours under a -0.095 to -0.098 MPa vacuum atmosphere in a vacuum drier to obtain a solid.
- the solid is cooled and pulverized to obtain surface-treated nano-TiO 2 particles.
- the surface-treated nano-TiO 2 particles are dispersed in the polyurethane pre-polymer by a high power supersonic dispersing machine to obtain modified polyurethane pre-polymer.
- the surface treated nano-TiO 2 particles are 1 to 3 wt % based on the weight of the polyurethane pre-polymer.
- the modified polyurethane pre-polymer is placed in a container A on a molding machine, heated to 70 to 82° C in a -0.095 to -0.098 MPa vacuum atmosphere and held still for 15- to 30 minutes to eliminate bubbles.
- the low molecular diol of the chain-extending agent is placed in a container B on the molding machine.
- the amounts of the polyurethane pre-polymer and the chain-extending agent are calculated by setting the chain-extending coefficient and the isocyanate group content.
- a pump connected to containers A and B draws proper amounts of the polyurethane pre-polymer and the low molecular diol from containers A and B.
- the treated internal rubber body is placed into a mold and pre-heated to 110 to 130° C. Then, the molding machine pours the polyurethane pre-polymer and the chain-extending agent into the mold. The mold is kept at a pressure of 0.2-0.3 MPa and a temperature of 110 to 130° C. After 30 to 80 minutes, the internal rubber body coated with the polyurethane tread is detached from the mold and placed in an oven to heat at 110 to 130°C for 12 to 24 hours to obtain a composite rubber tire with a polyurethane tread.
- the step of treating the outer surface of the internal rubber body (1) can be performed by treating the trimmed outer surface of the internal rubber body with a polyisocyanate surfactant.
- the trimmed outer surface is sprayed or coated with the polyisocyanate surfactant 1.5 to 12, or 1 to 8, hours before the act of applying the polyurethane pre-polymer (4) for molding.
- the act of improving the polyurethane pre-polymer (3) can be achieved by modifying the polyurethane pre-polymer with nano-particles of carbon white.
- the nano-particles of carbon white are 1 to 40 nm in diameter.
- a preferred diameter of the nano-particles of carbon white is 15 to 25nm.
- the nano-particles of carbon white are activated by heating and mixed well with a toluene solvent containing polyisocyanate at 80 °C for 1 to 2 hours.
- the polyisocyanate in the toluene solvent is 50 to 60 wt % based on the weight of nano-particles of carbon white.
- the toluene solution is 3 to 5 times the polyisocyanate.
- the toluene solvent is removed from the mixture by vacuum suction at -0.095 to -0.098 MPa at 220 to 240° C. Then, the mixture is dried for 4 to 6 hours, cooled and pulverized to obtain surface-treated nano-particles of carbon white.
- the surface-treated nano-particles of carbon white are dispersed in the polyurethane pre-polymer by a high power supersonic dispersing machine to obtain modified polyurethane pre-polymer.
- the surface treated nano-particles of carbon white is 1 to 3 wt % based on the weight of the polyurethane pre-polymer.
- the low molecular weight diol chain-extending agent in the act of preparing a polyurethane pre-polymer (2) is preferably selected from the group comprising: glycol, 1,4-butylene diol, and hydroquinone-bis( ⁇ -hydroxyethyl) ether.
- Step 1 treating an outer surface of an internal rubber body:
- An intermediate glue layer was attached to the outer surface of the internal rubber body. Then, the internal rubber body was vulcanized, trimmed at surfaces to which the polyurethane tread is applied and molded with the polyurethane tread.
- Step 2 preparing and improving a polyurethane pre-polymer:
- a "hydroxyl-terminated polybutadiene and 4,4'-diphenylmethane diisocyanate" system was prepared and nano-TiO 2 particles were used to modify the polyurethane pre-polymer.
- 100 PHR(Per-Hundred Resin) of hydroxyl-terminated polybutadiene with a molecular weight of 2000 was input into a reacting chamber, heated to 120 to 130° C until the hydroxyl-terminated polybutadiene melted and stirred in a vacuum of -0.095 to -0.098 MPa for 2 to 2.5 hours to dehydrate.
- the hydroxyl-terminated polybutadiene was cooled to 60° C, mixed well with 33 PHR of 4,4'-diphenylmethane diisocyanate, stirred and heated to 80° ⁇ 2° C for 2 hours to obtain the polyurethane pre-polymer.
- the surface-treated nano-TiO 2 particles were mixed well with the polyurethane pre-polymer by a high power supersonic dispersing machine to achieve the modified polyurethane pre-polymer.
- Step 3 molding a polyurethane tread on the internal rubber body:
- the modified polyurethane pre-polymer was placed in a container A on a molding machine, heated to 80° C in a -0.095 to -0.098 MPa vacuum atmosphere and held still for 10 to 15 minutes to eliminate bubbles.
- the chain-extending agent of 1,4-butylene diol was placed in a container B on the molding machine.
- the amounts of the polyurethane pre-polymer and the chain-extending agent are calculated by setting the chain-extending coefficient to 0.95.
- the treated internal rubber body with the intermediate glue layer was placed into a mold in a molding machine and pre-heated to 110° C. Then, the molding machine poured the polyurethane pre-polymer and the 1,4-butylene diol into the mold. The mold was kept at a pressure of 0.2-0.3 MPa and a temperature of 110° C. After 60 to 80 minutes, the internal rubber body coated with the polyurethane tread was detached from the mold and placed in an oven to heat at 110°C for 24 hours to obtain a composite rubber tire with a polyurethane tread.
- Step 1 treating an outer surface of an internal rubber body:
- a rubber radial tire was placed on a rotatable rack, trimmed at surfaces to which the polyurethane tread is applied and coated with polyisocyanate surfactant for1.5 hours before coating with the polyurethane tread.
- the rubber radial tire has to be coated with the polyurethane pre-polymer within 12 hours of applying the polyisocyanate surfactant and cannot be contaminated by water or dust on surfaces to which the polyurethane tread is to be applied.
- Step 2 preparing and improving a polyurethane pre-polymer:
- the nano-particles of carbon white were mixed well with the polyurethane pre-polymer by a high power supersonic dispersing machine to obtain the modified polyurethane pre-polymer.
- Step 3 molding a polyurethane tread on the internal rubber body:
- the modified polyurethane pre-polymer was placed in a container A on a molding machine, heated to 70 to 80° C in a -0.095 to -0.098 MPa vacuum atmosphere and held still for 15 to 30 minutes to eliminate bubbles.
- the chain-extending agent of glycol was placed in a container B on the molding machine. Amounts of the polyurethane pre-polymer and the chain-extending agent are calculated by setting the chain-extending coefficient of glycol to 0.98.
- the constant for glycol in the foregoing calculation formula is 0.738. Therefore, the pump connected to containers A and B was adjusted to prepare correct amounts of the polyurethane pre-polymer and glycol.
- the treated rubber radial tire with the polyisocyanate surfactant was placed into a mold in a molding machine and pre-heated to 120 to 125° C. Then, the molding machine poured the polyurethane pre-polymer and the glycol into the mold. The mold was kept at a pressure of 0.2-0.3 MPa and a temperature of 120 to 125° C. After 40 to 60 minutes, the rubber radial tire coated with a layer of polyurethane tread was detached from the mold and placed in an oven to heat at 120 to 125° C for 16 hours to obtain a composite rubber tire with a polyurethane tread.
- Step 1 treating an outer surface of an internal rubber body:
- An intermediate glue layer was attached to the outer surface of the internal rubber body. Then, the internal rubber body was vulcanized, trimmed at surfaces to which the polyurethane tread was to be applied.
- Step 2 preparing and improving a polyurethane pre-polymer:
- a mixture of 50 PHR of polytetramethylene glycol with a molecular weight of 2000 and 50 PHR of hydroxyl-terminated polybutadiene with a molecular weight of 2000 were input into a reacting chamber, heated to 125 to 135° C to melt and stirred in a -0.095 to -0.098 MPa vacuum atmosphere for 2.5 to 3 hours to dehydrate. Then, the mixture was cooled below 60° C, mixed well with 35 PHR of 4,4'-diphenylmethane diisocyanate, stirred and heated to 80° ⁇ 2° C for 1.5 to 2 hours to obtain the polyurethane pre-polymer. After cooling, a sample of the polyurethane pre-polymer was tested to determine the isocyanate group content.
- the surface-treated nano-TiO 2 particles were mixed well with the polyurethane pre-polymer by a high power supersonic dispersing machine to obtain modified polyurethane pre-polymer.
- Step 3 molding a polyurethane tread on the internal rubber body:
- the modified polyurethane pre-polymer was placed in a container A on a molding machine, heated to 70° C in a -0.095 to -0.098 MPa vacuum atmosphere and held still for 15 to 30 minutes to eliminate bubbles.
- the chain-extending agent of glycol was placed into a container B on the molding machine. Amounts of the polyurethane pre-polymer and the chain-extending agent were calculated by setting the chain-extending coefficient of glycol to 0.96.
- the constant of glycol in the foregoing calculation formula is 0.738. Therefore, the pump connected to containers A and B was adjusted to prepare correct amounts of the polyurethane pre-polymer and glycol.
- the treated internal rubber body with the intermediate glue layer was placed into a mold in a molding machine and pre-heated to 120° C. Then, the molding machine poured the polyurethane pre-polymer and glycol into the mold. The mold was kept at a pressure of 0.2-0.3 MPa and a temperature of 120° C. After 60 minutes, the internal rubber body coated with a polyurethane tread was detached from the mold and placed in an oven to heat at 120° C for 16 hours to obtain a composite rubber tire with a polyurethane tread.
- Step 1 treating an outer surface of an internal rubber body:
- a rubber radial tire was placed on a rotatable rack, trimmed at surfaces to which the polyurethane tread was to be applied and coated with polyisocyanate surfactant 7.5 hours before the polyurethane tread was applied.
- Step 2 preparing and improving a polyurethane pre-polymer:
- the surface-treated nano-TiO 2 particles were mixed well with the polyurethane pre-polymer by a high power supersonic dispersing machine to obtain modified polyurethane pre-polymer.
- Step 3 molding a polyurethane tread on the internal rubber body:
- the modified polyurethane pre-polymer was placed in a container A on a molding machine, heated to 80° C in a -0.095 to -0.098 MPa vacuum atmosphere and held still for 20 minutes to eliminate bubbles.
- the chain-extending agent of 1,4-butylene diol was placed in a container B on the molding machine. Amounts of the polyurethane pre-polymer and the chain-extending agent were calculated by setting the chain-extending coefficient of 1,4-butylene diol to 0.97. Therefore, the pump connected to containers A and B was adjusted to prepare correct amounts of the polyurethane pre-polymer and 1,4-butylene diol.
- the treated radial rubber tire with the intermediate glue layer was placed into a mold in a molding machine and pre-heated to 110° C. Then, the molding machine poured the polyurethane pre-polymer and 1,4-butylene diol into the mold. The mold was kept at a pressure of 0.2-0.3 MPa and a temperature of 120° C. After 60 minutes, the radial rubber tire coated with a layer of polyurethane tread was detached from the mold and placed in an oven to heat at 120° C for 16 hours to obtain a composite rubber tire with a polyurethane tread.
- Step 1 treating an outer surface of an internal rubber body:
- the internal rubber body was placed on a rotatable rack, trimmed at surfaces to which the polyurethane tread was to be applied and coated with a polyisocyanate surfactant by spraying or coating. After coating in 4 hours, the polyurethane tread was molded to the internal rubber body.
- Step 2 preparing a polyurethane pre-polymer:
- a purchased pre-polymer brand named Adiprene 8045 was obtained (purchased from Uniroyal company) and nano-particles of carbon white were used in this system to modify the pre-polymer.
- Step 3 molding a polyurethane tread on the internal rubber body:
- the modified polyurethane pre-polymer was placed in a container A on a molding machine, heated to 80° C in a -0.095 to -0.098 MPa vacuum atmosphere and held still for 15 to 30 minutes to eliminate bubbles.
- the chain-extending agent of 1,4-butylene diol was placed into a container B on the molding machine. Amounts of the polyurethane pre-polymer and the chain-extending agent were calculated by setting the chain-extending coefficient of glycol to 0.97. Therefore, the pump connected to containers A and B was adjusted to prepare correct amounts of the polyurethane pre-polymer and 1,4-butylene diol.
- the treated internal rubber body with polyisocyanate surfactant was placed into a mold in a molding machine and pre-heated to 127° C. Then, the molding machine poured the polyurethane pre-polymer and the 1,4-butylene diol into the mold. The mold was kept at a pressure of 0.2-0.3 MPa and a temperature of 120 to 125° C. After 60 minutes, the internal rubber body coated with a layer of polyurethane tread was detached from the mold and placed into an oven to heat at 120 to 125° C for 16 hours to obtain a composite rubber tire with a polyurethane tread.
- Step 1 treating an outer surface of an internal rubber body:
- An intermediate glue layer was attached to the outer periphery of the internal rubber body. Then, the internal rubber body was vulcanized, trimmed at surfaces to which the polyurethane tread was to be molded.
- Step 2 preparing a polyurethane pre-polymer:
- a hydroxyl-terminated polybutadiene and 4,4'-diphenylmethane diisocyanate system was used and nano-particles of carbon white were used in this system to modify the polyurethane pre-polymer.
- the surface-treated nano-particles of carbon white are dispersed in the polyurethane pre-polymer by a high power supersonic dispersing machine to obtain the modified polyurethane pre-polymer.
- Step 3 molding a polyurethane tread on the internal rubber body:
- the modified polyurethane pre-polymer was transported into a container A on a molding machine, heated to 80° C in a -0.095 to -0.098 MPa vacuum atmosphere and held still for 20 minutes to eliminate bubbles.
- the chain-extending agent of 1,4-butylene diol was placed into a container B on the molding machine. Amounts of the polyurethane pre-polymer and the chain-extending agent were calculated by setting the chain-extending coefficient of 1,4-butylene diol to 0.97. Therefore, the pump connected to containers A and B was adjusted to prepare correct amounts of the polyurethane pre-polymer and 1,4-butylene diol.
- the treated internal rubber body was placed into a mold in a molding machine and pre-heated to 110° C. Then, the molding machine poured the polyurethane pre-polymer and the 1,4-butylene diol into the mold. The mold was kept at a pressure of 0.2-0.3 MPa and a temperature of 120° C. After 60 minutes, the internal rubber body coated with a layer of polyurethane tread was detached from the mold and placed into an oven to heat at 120° C for 16 hours to obtain a composite rubber tire with a polyurethane tread.
- the composite rubber tire with a polyurethane tread has the following advantages.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Tires In General (AREA)
- Polyurethanes Or Polyureas (AREA)
- Tyre Moulding (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL04019085T PL1529788T3 (pl) | 2003-10-31 | 2004-08-11 | Sposób wytwarzania kompozytowej opony z bieżnikiem poliuretanowym oraz konstrukcji radialnej |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2003101119791A CN1325246C (zh) | 2003-10-31 | 2003-10-31 | 聚氨酯胎面-橡胶胎体复合结构绿色轮胎及其制造方法 |
CN200310111979 | 2003-10-31 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1529788A1 EP1529788A1 (en) | 2005-05-11 |
EP1529788B1 true EP1529788B1 (en) | 2007-07-25 |
Family
ID=34336323
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP04019085A Not-in-force EP1529788B1 (en) | 2003-10-31 | 2004-08-11 | Method for manufacturing a composite tire of polyurethane tread and radial carcase |
Country Status (7)
Country | Link |
---|---|
US (1) | US7524446B2 (ja) |
EP (1) | EP1529788B1 (ja) |
JP (1) | JP4007426B2 (ja) |
CN (1) | CN1325246C (ja) |
AT (1) | ATE368064T1 (ja) |
DE (1) | DE602004007738T2 (ja) |
PL (1) | PL1529788T3 (ja) |
Families Citing this family (27)
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CN1325246C (zh) * | 2003-10-31 | 2007-07-11 | 杭州悍马轮胎科技有限公司 | 聚氨酯胎面-橡胶胎体复合结构绿色轮胎及其制造方法 |
CN100415477C (zh) * | 2005-12-05 | 2008-09-03 | 广州华工百川科技股份有限公司 | 聚氨酯-橡胶复合轮胎的制造方法 |
CN100400314C (zh) * | 2006-01-27 | 2008-07-09 | 华南理工大学 | 一种聚氨酯实心轮胎及其制造方法 |
US20090183810A1 (en) * | 2008-01-23 | 2009-07-23 | Frederick Forbes Vannan | Newly manufactured airless or pneumatic tire having a reinforced rubber structure and a polyurethane tread |
US8151840B2 (en) * | 2008-01-23 | 2012-04-10 | Frederick Forbes Vannan | Method of manufacturing a new airless or pneumatic tire having a reinforced rubber structure and a polyurethane tread |
BRPI1006497A2 (pt) * | 2009-03-24 | 2019-09-24 | Dow Global Technologies Inc | prepolimero contendo grupos nco ativos, poliuretano ou poliuretano formados de uma composição compreendendo pelo menos um prepolimero, artigo metodo para fabricar um pneu borracha composito com uma banda de rodagem de poliuretano e pneu de borracha composito com banda de rodagem de poliuretano |
CN101648496B (zh) * | 2009-09-09 | 2012-03-14 | 杭州悍马轮胎科技有限公司 | 一种复合弹性体填充内腔的轮胎及其制备方法 |
NL2003748C2 (en) * | 2009-11-03 | 2011-05-04 | Apollo Vredestein Bv | Tire and method for manufacturing a tire. |
US8945688B2 (en) | 2011-01-03 | 2015-02-03 | General Electric Company | Process of forming a material having nano-particles and a material having nano-particles |
DE102011001303A1 (de) * | 2011-03-16 | 2012-09-20 | Continental Reifen Deutschland Gmbh | Kautschukmischung |
CN103031103A (zh) * | 2012-12-27 | 2013-04-10 | 广东达美新材料有限公司 | 一种保护膜用纳米改性水性聚氨酯压敏胶及其制备方法 |
CN103214686B (zh) * | 2013-04-17 | 2015-05-20 | 北京化工大学 | 双组份聚氨酯胶黏剂用于聚氨酯-橡胶复合轮胎的粘结工艺 |
US9180737B2 (en) | 2013-04-18 | 2015-11-10 | Caterpillar Inc. | Molded tire having different tread material |
CN103467975B (zh) * | 2013-09-12 | 2015-04-01 | 山东永泰化工有限公司 | 一种丁羟型聚氨酯复合轮胎胶料及其制备方法 |
CN103755907A (zh) * | 2014-01-22 | 2014-04-30 | 杭州台创实业有限公司 | 用于轮胎填充的浇注型聚氨酯弹性体 |
JP5864008B1 (ja) | 2015-05-08 | 2016-02-17 | サンユレック株式会社 | ポリウレタン樹脂組成物製造用ポリオール組成物 |
CN106366271A (zh) * | 2016-08-25 | 2017-02-01 | 浙江长兴宏诚橡胶制品有限公司 | 一种橡胶轮胎 |
WO2018112642A1 (en) * | 2016-12-20 | 2018-06-28 | Camso Inc. | Track system for traction of a vehicle |
JP6847523B2 (ja) * | 2017-03-14 | 2021-03-24 | 株式会社イノアックコーポレーション | ポリウレタン発泡体 |
CN108034224A (zh) * | 2017-12-19 | 2018-05-15 | 滁州环球聚氨酯科技有限公司 | 一种叉车轮毂表面包覆的聚氨酯层制备方法 |
CN108329456A (zh) * | 2018-01-17 | 2018-07-27 | 宁国市顺鑫金属制品有限公司 | 一种锻压机床缓冲垫及其生产方法 |
CN110467715B (zh) * | 2018-05-10 | 2020-10-02 | 北京化工大学 | 一种具有超低滚动阻力的丁二烯橡胶-聚氨酯弹性体材料及制备方法 |
WO2020249727A1 (de) * | 2019-06-14 | 2020-12-17 | Basf Se | Neue partikelschaumstoffe |
CN110437419A (zh) * | 2019-08-01 | 2019-11-12 | 栾川县新科机械设备修复中心 | 一种聚氨酯实芯轮胎充填料及其制备方法 |
CN112874241B (zh) * | 2021-01-16 | 2022-06-24 | 烟台辰宇汽车部件有限公司 | 聚氨酯-橡胶组合式轮胎以及用于该轮胎的聚氨酯材料 |
KR102586119B1 (ko) * | 2022-11-11 | 2023-10-06 | 주식회사 윌켐코리아 | 소음 저감 효과를 갖는 타이어 내부 폴리우레탄 발포체 분사 방법 |
CN117507442B (zh) * | 2023-09-28 | 2024-06-14 | 宁波伏龙同步带有限公司 | 一种双面齿同步带的制作方法 |
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ZA733319B (en) * | 1972-06-08 | 1974-04-24 | Firestone Tire & Rubber Co | Tire treads |
US3897386A (en) * | 1972-06-08 | 1975-07-29 | Firestone Tire & Rubber Co | Tire treads |
US4006767A (en) * | 1975-10-08 | 1977-02-08 | The Firestone Tire & Rubber Company | Pneumatic tires |
DE3124912A1 (de) * | 1981-06-25 | 1983-01-13 | Paul 4600 Dortmund Rösler | "verfahren zur runderneuerung von reifen und danach hergestellter reifen" |
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US4704176A (en) * | 1984-12-19 | 1987-11-03 | The Goodyear Tire & Rubber Company | Method of bonding polyurethane to cured rubber |
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DE3618251A1 (de) * | 1986-05-30 | 1987-12-03 | Dieter Schmermbeck | Verfahren und vulkanisationshuelle zum reparieren und runderneuern von fahrzeugreifen |
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GB9220131D0 (en) * | 1992-09-23 | 1992-11-04 | Compounding Ingredients Limite | Tyre tread |
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CN1174854C (zh) * | 2001-06-13 | 2004-11-10 | 广州华工百川自控科技有限公司 | 橡胶-聚氨酯弹性体复合结构绿色轮胎的制造方法 |
CN1325246C (zh) * | 2003-10-31 | 2007-07-11 | 杭州悍马轮胎科技有限公司 | 聚氨酯胎面-橡胶胎体复合结构绿色轮胎及其制造方法 |
-
2003
- 2003-10-31 CN CNB2003101119791A patent/CN1325246C/zh not_active Expired - Fee Related
-
2004
- 2004-03-16 JP JP2004074453A patent/JP4007426B2/ja not_active Expired - Fee Related
- 2004-06-23 US US10/875,672 patent/US7524446B2/en active Active
- 2004-08-11 AT AT04019085T patent/ATE368064T1/de not_active IP Right Cessation
- 2004-08-11 PL PL04019085T patent/PL1529788T3/pl unknown
- 2004-08-11 EP EP04019085A patent/EP1529788B1/en not_active Not-in-force
- 2004-08-11 DE DE602004007738T patent/DE602004007738T2/de active Active
Also Published As
Publication number | Publication date |
---|---|
JP2005132093A (ja) | 2005-05-26 |
US7524446B2 (en) | 2009-04-28 |
JP4007426B2 (ja) | 2007-11-14 |
US20050092424A1 (en) | 2005-05-05 |
EP1529788A1 (en) | 2005-05-11 |
PL1529788T3 (pl) | 2007-12-31 |
DE602004007738D1 (de) | 2007-09-06 |
CN1325246C (zh) | 2007-07-11 |
ATE368064T1 (de) | 2007-08-15 |
CN1539628A (zh) | 2004-10-27 |
DE602004007738T2 (de) | 2008-04-30 |
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